Method for producing emulsion polymerisates

Patent metadata

Field	Value
Publication number	US-2016208128-A1
Application number	US-201414913555-A
Country	US
Kind code	A1
Filing date	Aug 13, 2014
Priority date	Aug 22, 2013
Publication date	Jul 21, 2016
Grant date	—

Abstract

The present invention relates to a method of producing emulsion polymer particles having a core-shell structure wherein at least one polyalkylene oxide containing additive is used in the core, and also to their use in paints, paper coatings, foams, crop protection agents, liquid inks and cosmetic compositions.

First claim

1 . A method for producing emulsion polymer particles, the method comprising:
(i) performing a sequential polymerization to obtain a multistaged emulsion polymer in the form of particles; ii) neutralizing the particles with at least one base up to a pH of not less than 7.5; and iii) optionally polymerizing further shells comprising one or more nonionic ethylenically unsaturated monomer, wherein: the multistaged emulsion polymer comprises at least a core stage polymer and a sheath stage polymer; the core stage polymer comprises by way of polymerized units
from 5 to 99.5 wt %, based on the weight of the core stage polymer, of at least one hydrophilic ethylenically unsaturated monomer,
from 0 to 95 wt %, based on the weight of the core stage polymer, of at least one nonionic ethylenically unsaturated monomer, and
0.5 to 20 wt % of at least one nonionic polyalkylene oxide containing additive, based on the weight of the core stage polymer; and
the sheath stage polymer comprises by way of polymerized units not less than 50 wt % of a nonionic ethylenically unsaturated monomer.

2 . A method for producing emulsion polymer particles, the method comprising:
(i) performing a sequential polymerization to obtain a multistaged emulsion polymer in the form of particles; ii) neutralizing the particles with at least one base up to a pH of not less than 7.5, in the presence of not less than 0.5 wt % of a nonionic ethylenically unsaturated plasticizing monomer, based on the overall weight of the core-shell polymer; iii) subsequently polymerizing the nonionic ethylenically unsaturated plasticizing monomer optionally by further admixing one or more nonionic ethylenically unsaturated monomer; and iv) optionally polymerizing further shells comprising one or more nonionic ethylenically unsaturated monomer wherein: the multistaged emulsion polymer comprises at least a core stage polymer and a sheath stage polymer; the core stage polymer comprises by way of polymerized units
from 5 to 99.5 wt %, based on the weight of the core stage polymer, of a hydrophilic ethylenically unsaturated monomer,
from 0 to 95 wt %, based on the weight of the core stage polymer, of at least one nonionic ethylenically unsaturated monomer, and
0.5 to 20 wt % of at least one nonionic polyalkylene oxide containing additive, based on the weight of the core stage polymer; and,
the sheath stage polymer comprises by way of polymerized units not less than 50 wt % of a nonionic ethylenically unsaturated monomer.

3 . The method according to claim 1 , wherein the nonionic polyalkylene oxide containing additive is selected from the group consisting of a polysiloxane-polyalkylene oxide copolymers, such as polysiloxane-polyalkylene oxide graft copolymers of comb structure, polysiloxane-polyalkylene oxide graft copolymers of α,ω structure, polysiloxane-polyalkylene oxide graft copolymers having ABA or BAB block structures or further sequences of polyalkylene oxide polysiloxane blocks, branched polysiloxane-polyalkylene oxide copolymers, polysiloxane-polyalkylene oxide graft copolymers having polyester, (fluorinated) (poly)alkyl, polyacrylate side chains; copolymers of propylene oxide and ethylene oxide, block copolymers of propylene oxide and ethylene oxide, polyalkylene oxide-poly(meth)acrylate copolymers, polyalkylene oxide-(poly)alkyl copolymers, poly(alkylene oxide)-poly((meth)acrylate) block copolymer, fluorinated alkyl ester polyalkylene oxides and polyalkoxylates and highly branched polyalkylene oxides.

4 . The method according to claim 1 , wherein the nonionic polyalkylene oxide containing additive is selected from the group consisting of polysiloxane-polyalkylene oxide graft copolymers of comb structure, polysiloxane-polyalkylene oxide graft copolymers of α,ω structure or mixtures thereof.

5 . The method according to claim 1 , wherein the nonionic polyalkylene oxide containing additive is selected from the group consisting of polysiloxane-polyalkylene oxide graft copolymers of comb structure of general formula (I):

where
R1 to R9 are independently H or alkyl (—(CH 2 ) n CH 3 (n=0-20)) or OH or O-alkyl (—O—(CH 2 ) n CH 3 (n=0-20)) or allyl (—(CH 2 )—CH═CH 2 ) or O-allyl (—O—(CH 2 )—CH═CH 2 ) or phenyl or alkyl ester
n is 0-1000,
m is 1-100,
X is the following structure:

where
R10 is OH or O-alkyl (—O—(CH 2 ) n CH 3 (n=0-20)) or O-allyl (—O—(CH 2 )—CH═CH 2 ) or O-phenyl or an alkyl ester
R11 to R16 may each independently be H or alkyl (—(CH 2 ) n CH 3 (n=0-20)) or phenyl,
o is 0-100,
p is 1-100,
t is 0 or 2,
u is 0-10,
v is 0-10,
w, x, y, z may each be independently 1-10 and the same or different.

6 . The method according to claim 1 , wherein the nonionic polyalkylene oxide containing additive is admixed in amounts of 1 to 5 wt % of at least one nonionic polyalkylene oxide containing additive based on the weight of the core stage polymer.

7 . The method according to claim 2 , wherein the neutralizing ii) occurs under one of the following conditions (a-d):
(a) the plasticizing monomer does not homopolymerize, (b) in the presence of a plasticizing monomer having a ceiling temperature below 181° C., (c) after the polymerization has been stopped by admixing an inhibitor or a reducing agent, or (d) when the overall amount of the initiator is only up to 0.5 wt % of the sheath stage polymer and is admixed either before starting to mix the monomers of the sheath stage polymer or is only admixed during the first 50% of the monomer admixture of the sheath stage polymer.

8 . The method according to claim 2 , wherein the plasticizing monomer is selected from the group consisting of styrene, α-methylstyrene, vinyltoluene, ethylene, butadiene, vinyl acetate, vinyl chloride, vinylidene chloride, acrylonitrile, acrylamide, methacrylamide, (C 1 -C 20 )alkyl or (C 3 -C 20 )alkenyl esters of acrylic or methacrylic acid, methacrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, butyl methacrylate, 2-ethylhexyl acrylate, 2-ethylhexyl methacrylate, benzyl acrylate, benzyl methacrylate, lauryl acrylate, lauryl methacrylate, oleyl acrylate, oleyl methacrylate, palmityl acrylate, palmityl methacrylate, stearyl acrylate, stearyl methacrylate, esters of 2-phenylacrylic acid/atropic acid (e.g., methyl, ethyl, n-propyl, n-butyl), 2-methyl-2-butene, 2,3-dimethyl-2-butene, 1,1-diphenylethene, 1,2-diphenylethene, methyl 2-tert-butylacrylate and maleic anhydride.

9 . The method according to claim 2 , wherein the nonionic ethylenically unsaturated plasticizing monomer is maleic anhydride, stilbene or α-methylstyrene.

10 . The method according to claim 2 , wherein the nonionic ethylenically unsaturated plasticizing monomer is selected from the group consisting of α-methylstyrene, esters of 2-phenylacrylic acid/atropic acid (e.g., methyl, ethyl, n-propyl, n-butyl), 2-methyl-2-butene, 2,3-dimethyl-2-butene, 1,1-diphenylethene and methyl 2-tert-butylacrylate.

11 . The method according to claim 1 , wherein the average particle size in the unswollen state of the core stage polymer, comprising seed and swell-seed, is in the range from 50 to 300 nm.

12 . The method according to claim 1 , wherein the glass transition temperature, determined by the Fox equation, of the core stage polymer in the protonated state is between −20° C. and 150° C.

13 . The m

Assignees

• Basf Se

Inventors

• Kehrloesser Daniel
• Leswin Joost
• Specker Daniel
• Roschmann Konrad
• Gerst Matthias
• Wiese Harm

Classifications

• C09D151/00

  Coating compositions based on graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds (based on ABS polymers C09D155/02); Coating compositions based on derivatives of such polymers · CPC title

• C08F2/22

  Emulsion polymerisation · CPC title

• B01J13/16

  Interfacial polymerisation · CPC title

• C09D5/02

  Emulsion paints {including aerosols} · CPC title

• C08F265/06 Primary

  Polymerisation of acrylate or methacrylate esters on to polymers thereof · CPC title